Julius j



(No Model.) A I J. J. SUOKERT. METHOD OF AND APPARATUS FOR GOMPRESSING AND LIQUEFYING GASES AND PRODUGING REFRIGERATION.

N0.302,294. P tented 111 2 2, 884

UNITED STATES PATENT OFFICE.

JULIUS J..SUCKERT,- OF BIDGEWOOD, JERSEY.

METHOD OF AND APPARATUS FOR COMPBESSING #ND LIQUEFYING GASES AND PRODUCING REFRIGERA- ION.

SPECIFICATION forming part of Letters Patent: No; 302,294, dated-July 22, 1884.

- Application died December 13, 1883. (No module To all whom it may concern:

Bait known that I, JULIUS J. Scanner, a citizen of the United States, residing at Ridgewood, in the county of Bergen and State of 5 New Jersey, have invented new and useful Improvements'in Method of and Apparatus for Compressing andl iquefying Gases and Producing Refrigeration; and 'I do hereby declare that thefollowing is a full, clear, and r exact description of the invention, which will enable others skilled in the art to which it ap'pertains to make and use the same.

Heret'ofore those using a sealing or lubricating liquid for sealing the piston and valves'of a compressor and for lubricating itsmovable parts have either introduced such liquid into the compressor through its suction-inlets e11 tircly free from gaseous pressure, orat a press-' are not exceeding the pressure of the gas entering the suction or inlet valve of the compressor, or-the liquid has been introduced at the li quefying pressure of. the gas into a cham-' her or pipe comparatively free from pressure,

or wherein the pressure is not in excess of that 2 5 of the gas on the suction side of themachin'e,

- and where an equalization of pressures takes place before the liquid is introduced into the cempre'ssion chamber; In consequeuce'of the reduction of pressure, the gas absorbed by the liquid at'a higher pressure, 'escapes'ifrom it,

necessitating the-recompressionof the escaped gas without its having performed work; therefore; such an apparatus fails to perform its maximum work.

The object of thisinvention is to discharge uid is charged for the absorption of the heat of compression, or -a part thereof, therebyreducing the work of" compression; and to diminish the quantity of liquid required for db.

5 stracting the 'heat' of compression} and to avoid the lossof etliciency caused by allowing the gas with which the sealing or lubricating liquid is charged to escape to the suction or expat ion sideof the apparatus or into a 5: chamber of the compressor before it has been froni a gas'co n'prcs'sor a greater quantity of supplied with its full complement of gas,

in this way not only lose the cooling efiect which may be produced by the-vaporization of the gas released from thesealiug or 1ubricatingliquid when injected during the act of compression,-but also the loss occasioned by being compelled to recompress the gasescaping from the sealing or lubricating liquidwithout its having performed work. This loss-of efliciency, caused by the escapeof gas from the sealing orlubricating liquid, increases as the. pressure. to which the gas is'compressed'increases, for the volume of gasabsorbcd by the sealing or lubricating liquid increases directly. with the pressure exerted upon it. i

The introduction of a sealing or lubricating liquid ha's hitherto been attaiued only at considerable loss in efiiciency, which is 'iudifierentlyshown by an indicator diagram or card taken from ammpresscr such lubricat- 7o ing liquid, but becomes plainly apparentwhen the actual quantity of gascompressed and liquefied is found, by weightor computed by volume, which shows the loss of efliciencyte" be from thirty to fiftyper cent.- Aloss of this 7 5 nature can only be avoided by using asealing orlubricating liquid charged with gas or liquefied gas under a pressureexceeding that of the gasfentering. the qompressorto'bc compressed, and by injecting such lubricating 8o liquidso charged with gas into the compressor during the-act of compression, or after the compressor has received its full complement of gas. By this means, no matter whatamoimt Y of gas or liquefied gas the sealing or lubricating liquid may contain prior to its introduc tion into the compressor, if itspressure be at all in excess of the pressure of the gas on the suction side, the percentage of gas enteringthe compressor and discharged increased aboqe that of all othersystemswheie in a sealing or lubricating liquid is used in proportion as the amount of gas which the lubricant contains under a pressure is in" excess of the pressure on the suction side.,. To 5 make this more apparent, state that the primary object in introducing a liquid into a compression pumpwas to seal thevalve'sand fill the waste spaces of the pump. Theseu- 'ondary object was the lubrication of the ,workj: 7

ing parts. The volume of liquid used in the flrst+known cascof kind-was andf 1 t erefrom wilhbe 9o the result was that the liquid absorbed so great a quantity of gas under the pressure exerted that the pumps were abandoned as impractical. Similar attempts have been made since and have also been abandoned, for the same reason, .that the liquid absorbed such a large quantity of gas during the act of compression that upon the return-stroke of the piston and a reduction of the pressure the gas escaping from the liquid'into the chamber of the compressor entirely filled it, and under sufficient tension to prevent the gas on the suction side from entering the pump. The result was a failure to pump and discharge the gas.- The quantity of this liquid was then reduced with more satisfactory results; At this period the knowledge attending the compression of gases had reached a point where engineers could clearly demonstrate that the heat generated by the compression of a gaseous body, if not abstract-- ed, resulted in a loss of power in consequence of the expansion .of the gas by the heat developed during compression, and this was clearly shown by applying an indicator to thefcompressor. The cards taken made it apparent that a gas being compressed without means of abstracting the heat followed the adiabatic instead of the isothermic curve. Means were then employed for abstracting the heat of compression by circulating and cooling the sealing and lubricating liquid, and by injecting a quantity of such cooled liquid into a chamber or pipe connected with the suction side of the compressor at each stroke oithe compressor; but it was found necessary to do this without exposure to the'atmosphere; to avoid the loss ofexpensive gas, except in the case of the compression of atmospheric air. Thus far the improvements were a great gain but even withthe improved system of introducing a smaller quantity of cooled lubricating-liquid and circulating it without exposnreto the atmosphere a great loss still exists, which, in spite of the experience gained by former investigators,- has not heretofore been overcome.

Before proceeding with further explanation I will state that the compression of gases underordinary conditions is subject to-the established law of Ma'riotte, except so far. as this law may be modified by that of G'ay-Lussac, and it will make no special-dillerence what the initial and final pressures of the gas to be compressed are, as the volume of the gas will al ways be inversely as the pressure, and'vice versa. Another important thingto be remembered is that liquids absorb more or less gas, according to the pressure and. temperature to which they are exposed. For instance, water will absorb seven hundred times its volume of ammonia-gas at atmospheric pressure and at Fahrenheit; other liquids a proportiom ate amount, according to their aflinity for the gas with. which they may be in contact. w

As a matter of convenience, and to make this statement clear, I will assume that the compressor contains one thousand cnbicinches of gas which is admitted thereih at atmospheric pressure, or fifteen pounds per square inch. Forthis proportion of gas in the compressor, say I admit twenty cubic inches of sealing or lubricating liquid which will absorb more than fifty cubic inches of gas at the pressure of the atmosphere. If this liquid be exposed to gas or liquefied gas under ap'ressure of one hundred and fifty pounds per square inch, it will, following a well-known physical law, absorbfifty cubic inches of gas at this pressure; but this volume of gas would expand to five hundred cubic inches if the pressure were reduced to that of the atmosphere. Now, it will be apparent, if the lubricant has been exposed to or charged with gas, as above described,'and then discharged into a tank or receptacle which is under the working pressure of the pump, that upon its reintroduction into a compressor or the pipes or chambers connecting therewith wherein areduced pressure exists only equal in the instance given to that of the suction side, four hundred and fifty cubic inches of the gas will. escape from the liquid,leaving fifty cubic inches still absorbed. There must consequently be an absolute waste of power and time required to recompress the four hundred and fifty cubic inches of gas es-' caping from the lubricating-liquid discharged from the compressor at each stroke of its piston. Therefore, instead of discharging one thousand cubic inches of gas at each stroke of the compressor, estimating it at atmospheric pressure, but five hundred and fifty cubic inches are discharged in a utilizable form, the remaining four hundred and fifty cubic inches being retained by the lubricating-liquid and permitted to escape to the suction side of the machine without performing work, which in the above examplewouldresult in a loss of efficiency of forty-five per cent. To attain this result, it is assumed in the foregoing statement that the same temperatures and-the same conditions exist throughout the operation. Practically these vary, and such variation would varythc above figures; but the final result ap proximates to that attained in actual practice. By introducing the-sealing or lubricating liquid-charged with gas or liquefied gas under the working pressure according to the present improvements, the above loss is entirely obviated. In additionthereto,anotheradvantageisgained by'utilizing the heat-absorbing qualities of the gas dissolved in the lubricating-liquid by its escape from the liquid when exposed to a reduc'ed pressure, which will be the case when the liquid is introduced charged with gas undcr the working pressure into the compressor at the beginning or during a portion of the compression-stroke, andas the pressure within the compressor increases during compression, a point will be reached when the pressure is equal to the pressure at which the liquid was charged with gas-i. 0., the working pressure. Npw, if no increase of temperature occurs above thatatwhichtheliquidischarged,

no gas will escape; but practically this is not the fact. The temperature increases to some extent. Therefore,even atthis point, the increase in temperature still continues to expel some gas from the lubricating-liquid, whereby the heat developed continues to be' taken up. By injecting the lubricating-liquid charged with gas in the manner above stated, more heat will be abstracted by the same volume of lubricating-liquid than by the old method, or smaller volume of the lubricating liquid charged with gas will be sufiicient to abstract the greater portion of the heat developed by compression; and,again,theproportionateamountofheat abstracted by this method will cause the compression-curve to approach closer to the isothermic than has hitherto been eflected, show ing a resulting economy in power. It is thus evident that a great advantage is gained over the old system by introducing the sealing or Iubricating-Iiquid into the chamber of a single-acting pump having its full complement of gas when the said sealing or lubricating liquid ischarged with as or liquefied gas, and both the lubricatingiquid and gas are introduced under a pressure equal to the liquefyingpressure of the gas, or a pressurein'excess of that of the gas entering the suction-inlet'of the compressor to be compressed but the gain is great- ,er when the liquid isinjected during the act of compression. The cooling action efiected by theexpulsion or vaporization of the gas or liquefied gas from the sealing or lubricating-liqa portion of the heat generated during the act of compression, can beincreased or diminished by using difierentsealing or lubricating agents which have more or less aflinity or absorbing capacity for the gas or liquefied gas with which they come in contact. The absorption of the gas by the sealing or lubricating liquid can be increased by cooling the lubricating or sealing liquid in contact with the gas, ort of gas absorbed can be diminished by simply returning the lubricating or sealing liquid'to the compressor without cooling. Again, the quantity of sealing or lubricatin liquid can be injected into the compressor 1n predetermined quantifies by means of a pump 'or other device; or it may be allowed to flow into the compressor by the prwsure exerted by a column of the liquid, and be controlled by means i of suitable valves which may be opened and "without exposure to the atmosphere, and'then,

closed automatically.

To these ends the invention consists in the process by which the efliciency of a gas-compressing apparatus is increased, which process consists in circulating a sealing or lubri-Y eating liquid and exposing the said liquid to or charging it with gas or liquefied gasunder.

a pressure exceedingzthe pressure of the gas entering thecompressor to be compressed, and v injecting the said sealing or lubricating liquid while so charged with gasand under such press are into a chamber of u gas-compressor supe quantity plied with its full 'complemcnt'of gas, either prior to or during the act of compression, as will hereinafter appear.-

The-invention also consists in the process by which the efliciency of a gas-compressing apparatus is increased, which process-consists eating liquid and exposingthe said liquid to a pressure exceeding the pressure of the gas entering the compressor to be compressed and without-exposureto the atmosphere, and then injecting such sealing or lubricating liquid while so charged with gas and undersuchpressure, in predetermined quantities, into-a chamber of a gas-compressor charged'with its full complement of gas, either prior *toor during the act of compression, and then absorbing the heat'of compression ora part thereof within the compressor by the release and expansion of the gas. held by the sealing and lubricating liquid when injected, as willhereinafter appear. 4

The invention also consists in the process apparatus is increased, which process consists in circulatingilndcooling a sealing or lubriphere,.exposing the said liquid to or charging it with gas or liquefied gas under apressure exceeding the pressure of the gas entering the compressor to be compressed, and then injecting such sealing or lubricating liquid while so charged with gas and without reducing its pressure into a chamber of a gas-compressor supplied with itsfuil complement of gas, either prior to or during the act of compression, as will hcreinaiter appeara The invention also consists in an improved gas-compressor having a peculiar construction and arran gementof valves and ing or lubricating liquid under pressure is prevented from entering the compressing-cylinder during thesuction-strokeot' the compressor-piston, as will hereinafter appear.

. Theinvention also consists in an improved gas-compressor having a peculiar construction and arrangement of valves and parts, whereby or lubricating liquid under pressure is prevented from entering the com-pression-cyliuder during the suction-stroke of the com presjsion-piston, but which admits the said liquid to the compression-cylinders during the act of compression, as will hereinafter appear.

The. invention also consists in a gas-compressor having a liquid-pump in combination therewith, the wh ole constructed and arranged so that the said compressor, when? connected with, a, gas-condenser and a liquid-reservoir,

upon its outer side by a liquid under pressure, y as will hereinaiterappear. i

' Theiuvention also consists ofthecomhination in circulating and cooling a sealing or lubri-v or charging it with gas or liquefied gas under' eating liquid without exposure to the atmos- I parts, whereby the said valves are held in place and a sealby which the efiiciency of a gas-compressing.

the said valves are held in place anda sealing has its valveslliquid sealed, and the piston-rod ,orifice in the head of the compressor is sealed i of a gas-compresser and auxiliary pump,when

constructed and arranged so that the piston of the compressor and the piston of the auxiliary pump shall have a common piston-rod,

- and the piston-rod and its orifice in the head and the conduits and connections shown and described, as will hereinafter appear; and the invention also consists in combinations of mechanisms and devices shown, described, or used for effecting the desired process, as will hereinafter appear One practical embodiment of theseim'provements is-illustrated in the accompanying drawing, the same showing an elevation, partly in section, of an apparatus \which will now be fully explained.

A and A are the compression-chambers of a double-acting compressor, 3. aisthe main piston of the eompressor,having a long piston-rod, a, upon which is secured a smaller piston, a which moves within the chambers b and b of an auxiliary pump, C,

' that is used to inject the sealing or lubricating liquid into the chambers A and A of the compressor. This pump, when charged with its supply of lubricating-liquid, forms a seal under pressure; and prevents gas from leaking from the compressor during the act of compression.

yaud y 'are grooves entirely surrounding the piston a, and communicating'with the chambers A and A bymeans of the orifices a; and x, to serve as a--receptacle for a lubricatingliquid which prevents the gas from slipping past the piston during the act of compression. The pistons, as showh' in the drawing, are supposed to be moving inthe direction pointed by-the arrow.

c is the gas-inlet valve of the chamber A, shown as closed, and'c is the gas-inlet valve of the.chamber 'A, shown as" open.

02 is the gas-discharge valve of the chamber A, shown as open, and dis the gas-discharge valve of the chamber A, shown as closed. Like valves-es the companion, induction, and. eduction valvesare connected by a chamber upon that side of the pump where the said valves are located, one of which chambers-P- namely, that connecting the induction-valves c and c'-has communicating with it a large suction or gas-supply pipe, D, while the other ehambernamely, that connecting the eduction-valves d and dcommunicates with a large discharge-pipe, E, and the latter connects with the coolerF and condenser G.-

H is the reservoir for receiving the sealing or lubricating liquid and the liquefied gas, which are kept continuously under a pressure equal to that of the working pressure of the apparatus. I

I is an expansion soil for 'cooling, wherein the liquefied gas is expanded for the absorption of heat. The liquefied gas is admitted from the reservoir H .to the said coil through the pipe e and stop-cock e f is the pipe conveying the expanded gas from the expansion-coil back to the compressor, and connects with or forms part of the main suction or return gas pipe D.

- h is a pipe connecting withothe reservoir 11,-

to supply the auxiliary pump with lubricating or-sealing liquid through the pipe h. It also connects with a pipe, h, which supplies the piston-chamber 1, of the valve 3' with a column of liquid which is under the working pressure of the machine, and as-the piston of the valve j has a greater area then its valve-seat, and'both. are under the same working pressure, such pressure insures'the' seating of the valve j, and holds it in position when the main piston a i moving in the direction pointed by the arrow, thereby preventing the liquid entering the chamber 1; of the auxiliary pump 0 under the working pressure from forcing its way through the valve j into the chamber 'A upon the suction stroke of the compressor. The pipeh alsoconnects through apipe, h, with the chamber 1', at the dischargevalve j", and supplies said chamber with a column of the l'ubricatingliquid under pressure. Both discharge-valves j and j of the auxiliary pump 0 have stems or rods which connect with pistons of a larger area than the seats of the valves.- These pistons move in the chambers i and t, and each having upon its upper surface a column of the lubricatingliquid under the working pressure of the ma-- chine, they will by reason of this excess or area under pressure he firmly heldto their seats -during the suction-strokes of the piston a, thus preventing the introduction of the sealing or lubricating liquid into each chamber of the compressor until the said chamber is charged with its full complement of gas and the act of compression begins. The pipe h has'a continuation, h, that communicates with the piston-chamber i" of the valve 9" and supplies a column of lubricatingliquid under the working pressure of the machine, and which acts in a similar manner upon this ,valve as upon the valve j. under like conditions; but it willbe observed that the valve ,7 is held open during the'act of compression, or while the piston ais moving in the direction pointed by 120 ing or lubricating liquid passes under press-vure either; from the reservoir H or the pipes t the'avrow,-in the following manner: The seala" and-the port r (shown iii-part by dotted lines) to the corresponding connecting-pipes s ands-tothe'discharge-valves j and j".

As shown in the drawing, the auxiliary pump-piston a is exampled as moving in theer k,below the suction valves m r direction pointed by the arrow, and the sealing or lubrieatingliquid is entering the valve m and its corresponding port into the chamber b. The liquid contained in the chamber b is being forced through the port r, the connecting-pipe s, the discharge-valve j, and the apertures at a into the chamber A in the form of jets or spray during the act of compression,

the pressure upon the liquid. discharged being sufliciently in excess of the working pressure to overcome the resistance exerted by the difi'erencc'in the area of the discharge-valve j and its piston i". This excess of pressure is also exerted upon thesuetion-valvc m, there by keeping it closed during the discharge of the liquid from the chamber b; but it will be apparent that the sealing or lubricating liquid cannot enter the chambers of the compressing-pump B until the pump has received its full complement of gas and the act of compipe 0. Another advantage in having the chamber N connected with the expansion or return pipe f is that sometimes, when working the pump with great rapidity,.it becomes very warm, particularly its piston-rod, owing to tight packing, and insueh cases the'cold return-gas can be introduced into the pump by opening the cock iii the pip eo,and its parts thus be. cooled. The continuatiouof the discharge-pipe E is surrounded by a casing, T, of greater diameter than the pipe, and having its lower end closedby a bushing or reducing closure around the pipe E, forming a tight joint. Its upper end can communicate with the condcnscrG, if necessary, by opening the valve R. The pipe U, having the stop-cock u, conveys, the gas [mm the annular space formed by the casing T, surrounding the pipe E,"to the vertical cooler F, thence through the collect said cooler. and discharges it into the vertical pipe t, while the sealing or lubricating liquid separated at this point passes through the pipe t and valve 1 to the liquid supply pipe h. The gas, withsuch portions of the sealing or lubricating liquid as may not be condensed, is driven upward through the ipe t into'thc .coils of the condenser G. ater passing over these coils in thin streams absorbs the heat developed by the compression of the gas and the vaporized sealing or lubrieating liquid, causing both to liquefy and follow the course of the coil and empty through the pipe 1: into theliquid-reservoir H, where,

by reason of their different specific gravities, the scaling orlubricatiug liquid, being heavier, will settle to the bottom, and may be drawn through the pipe h and valve p, and the liquetied gas be drawn from the top through the pipe e. If the lubricant is lighter than the gas, an arrangement of parts may be readily made to reverse this part of the operation. The sealing or'lubricating liquid separating in the annular space formed between the pipe E and easing T may be drawn, priorto its entrance into the cooler F, through the pipe q into .the pipe h by opening the valve q, and be thus supplied .warm to the auxiliary pump 0, if occasion shouldso require. A

gage, 10, may be provided to show the quantity of the liquids in the liquid-reservoir H.

Before describingthe operation I will designate two parts of the apparatus bythe appellations usually applied in practice to them. From the cock e in the pipe c to the inletvalves of the compressor is known as either the expansion, suction, or return side of the apparatus,while the remaining portion ofd the apparatus is called the pressure si e. Having described the various parts of the apparatus, it may be observed that any volatile liquid or as may be used; but while ammonia is pre erred, sulphur dioxide, methylamine, carbonic acid, 820., may be employed, while the sealing or lubricating liquid maybe oil, glycerine, or any other suitable to the purpose of sealing or lubricating.

The apparatus being fully provided with the necessary gas and the proper supply of sealing or lubricating liquid, the operation will be as follows: Upon the movement of the main piston in the reverse direction to thatindicated by the arrow, the chamber A is charged with its full complement of gas, which enters the chamber by the lifting of thesuction-valve c. The piston a of the auxiliary pump, moving simultaneously in the same direction,d-raws the sealing or lubricating, liquid through the entrance-valve m'"and fills the chamber b, the port r, and the connecting-pipes. The stroke being new reversed, both pistons move in the contrary direction, or in that indicated by the arrow, and the piston a compresses the gas in the chamber A, and the piston it forces the sealing or lubricating liquid from,the chamber bthrough its outlet-port r and connecting pipe s with suflicient pressure to open the discharge-valve j, notwithstanding the excess of area of the piston of that valve, and injects the sealing or lubricating liquid through the apertures at n in the form of spray or a series of jets into the compression-chamber A, the discharge'coutinuing as-long as the piston a moves in such direction. The sealing or Inbricating liquid charged with gas or liquified gas under pressure, upon its entrance into the compression-chamber A. at a period when the pressure within said chamber is below that at which the said'liquid was charged, parts with ICC IIO

a portion of the gas or liquefied gas held in solution, or with which it is charged, thereby reducing its own temperature as well as that oi the gas being compressed. As the main piston a advances and the pressure within the compression-chamber A approaches that at which the sealing or lubricating liquid was charged with gas or liquefied gas, the heat dcvcloped-by compression is in great part spent in increasing the temperature of the sealing or lubricating liquid and the absorbed gas or liquefied gas injected with it, thereby expelling a portion of the latter, and by this means the power required. to perform the act of compression is materially reduced. .The pressure within the compression-chamber A having in the meantime reached that in the condenser G and the chamber leading from the dischargevalve, the discharge-valve d is opened and the gas escapes through the discharge-pipe E and the cooler F to the condenser G, where it is liquefied and flows into the reservoir H, and is ready for any use to which it may be desirable to apply it. The sealing or lubricating liquid is partially discharged in thewform of foam or vapor with the gas. Thatremaining in the chamber A fills the waste spaces formed between the valve j, the suction-valve c, the

' dischargc-valie d, the compressor-head Z, and

the piston a. Any excess thereof being forced past the discharge-valve d, effectually seals the same when it closes, and is carried by the gas with that which has already passed off in the form of foam or vapor through the dischargepipe E, and either settles in the annularspace formed by the pipe E and easing T, or it passes into the cooler F, and thence flows into the pipet, or it is carried through the pipe't and the condenser. G to the liquid-reservoir H. A portion of the sealing .or lubricating liquid also enters the' orifice w, and fills the groove y surrounding the piston, and seals the same, and, if a-lubricating-liquid is used, also lubricates the piston and other moving parts. Upon the return-stroke of both pistons the same operation isrepcated in chamber A of the compressor, and in chamber b and portr of the auxiliary pump, and in pipe 8' and dischargevalve j. Assuming that the return-stroke is being performed, the discharge-valve d of the chamber A immediately closes and is sealed by the liquid covering it, the suction-valve c isopened, and gas enters the chamber through the liquid covering the suction-valve c. The pressure required to open the value)" being in excess of that exerted by the piston'i'. it follows that u pen the return-stroke of the auxiliary-pump piston a" the valve is relieved of this excess of pressure, and is immediately closed by the pressure of the liquid or liquid and gas exerted upon the piston 1'. At the same moment the inlet or suction valve-m of the auxiliary pump again opens, and the operation as previously described '5 repeated. When the compressor is operat ng, the sealing or lubricating liquid and the gas are usually circulating under the pressure exerted by themach1ne,designated here as the work-- 111g pressure, which will average, say, about one hundred and fifty pounds to the square with this apparatus it is intended that while the lubricating-liquid and gas or liquefied gas are combined, which is throughout the pressu re side of the machine, they shall be under the working pressure, except during that portion of time when the gas in said liquid is expending in the cylinder of the compressor during the act of compression, or at a time when something outside of the usual order occurs. Consequently,when the lubricating or sealing liquid is introduced'into the compressor, it is always charged with gas or liquefied gas undcr a pressure in excess of the pressure of th: gas entering the compressor to be compressed. In case the pump is used for producing a vacuum, or the expanding gas from'the coil I is returned-with -suffic ent rapidity to C0!)- g'eal the sealing or lubricating liquid within the pump, it-may be necessary to nse'the warm sealing or lubricating liquid accumulating' in the annular space between the pipe E and easing T, which can be done by opening the valve 9, thus allowing the fliquid to flow through the pipe gf to the pipe h, and thence 430 the auxiliary pump; or it may be necessary to use the liquid passing through the cooler F and accumulating in the pipe t, which may be done by opening the valve p; or the liquid may be used from the reservoir H by opening the valve 1) in pipe h. By prop- .erly regulating the quant ty of sealing or lubricating liquid entering the auxiliary pump 0 by means of the valves q, p, or p, the heat of compression can beincreased or diminished at will; or the sealing or lubricating liquid can be injected into the compression-chamhere A and'A during any portion of the compression-stroke. If the auxiliarypump is .sllowed to fill its chambers b and b entirely with thesealing or lubricating liquid, the discharge of the same into the compressing-chambers A and A will be simultaneous with andpcntinnous during the period of compression and the discharge of the compressed. gas. By redncing the flow of .thc sealingorlubricatmg liquid to the auxiliar pump 0 by means of.

7 reached its maximum compression and is be gas-compressing 3o same consisting in circulatinga sealing or Iming forced through the 'discharge-outletsof the compressor.

from the compressor at each stroke of the pis ton will be in gaseous form and can be utilized. Thus'it will be apparent that by this proccss nearlyas much gas can be compressed at one stroke of the piston as can be compressed by two strokes under other systems previously described, and that the increase of efiiciency is of great value'in the com prcssion and liquefaction of gases.

As the condenser herein shown formstne subjccbmatter of another application, no specific claim to the elements of invention which it embodies is herein made; but,

I Iaving described my invention, what I claim i's-' 1. The process by which' the etficiency of a apparatus 'is' -increased, the

bricating liquid, exposing the-said liquid to or charging itwith'gas or liquefied gas under a pressure exceeding the pressure of the gas entering the comprcssorto be compressed, and then injecting the said sealing or'lubricating liquid while so charged with gas and under such pressure into a chamber of a gas-compressor supplied with its full complement of gas, either prior to or during the act of compression, all without exposure to the atmosphere. substantially-as described.

2. The process by which the efficiency of a gas-compressing apparatus is increased, the same consisting in circulating and cooling a scaling .or lubrieatingliquid, exposing the said liquid to or. charging it. with. gas or liquefied gas-under a pressure. exceeding the pressure of the gas entering the compressor to be compressed, and then injecting such sealingor lubricating liquid while so charged "with gas and under such pressure into a chamber of a gas-compressor supplied with its full complement of gas, either prior to orduring the act of compression, all without exposure to 'the atmosphere, substantially as described.

3. The process by which the efliciency of a gas-compressing apparatus is increased, the same consisting in circulating and cooling-a sealing or lubricating-liquid, exposing the said liquid to or charging it with gas or liquefied gas under a pressure exceeding the pressure of the gas entering the compressor to be cornpressed, then injecting such sealing or lubrifcating liquid while so charged with gas and under such pressure -'in predetermined quantities into a chamber of a gas compressor H -Again, assuming that the, compressor, when charged with its full comcharged with itsfnll complement'of gas, and then absorbing the heat of compression, ora part thereof, within the compressor by the release and: expansion of thegas held by the sealing 'or lubricating liquid when injected, all without exposure to, the atmosphere, substantially as described ,4. In a gas-compressor, the combination. with the pistou-rod thereof and an external chamber in which said piston-rod works, of an auxiliary pump provided with suitable valves and connecting-pipes, whereby a sealing or lubricating liquid is introduced into said chamber, and thereby seals said pistonrod, substantially as described.

,5. Tile combination, with a gas-compressor having an external chamber connected with or attached to its-head, through which chain-.- bcr a piston-rod works,and in which a sealing or lubricating liquid is introduced toseal the piston rod, of an auxiliary pump provid-' ed with suitable valves and connecting-pipes. whereby the'said liquid is introduced within the compression-chamber of said compressor when fully charged with gas, substantially as described.

6. The combination, with the piston-rod of a gas-compressor, of an-aux iliary pump, "the liquid chamber whereof operates as a sealingchambcr for the piston-rod of the gas-compressor outside of said compressor, substantially'as described. I

7. The combination, with a gas-compressor and an auxiliary pump-having suitable valves and condl its, whereby aliquid is introduced from said' pump into the compressor, ofa piston-rod common to both, moved by the pump seals the piston-rod upon the outer sideof the compresso'nhead, substantial] y as described,

8. The combination, with a gas-compressor and an auxiliary pump having a. piston-rod common to both, of suit-able valves and cond-uits arranged to introduce aliqui d from said pum'p into the compressor, substantially as described.

9. The combi'natiomwith a gas-compressor, of an auxiliary pump, the liquid-pumping chamber whereof is constructed, connected, and arranged to form' a chamber, in which gas escaping through the piston-rod orifice in the head of the compressor-is arrested, substantially as dc'scribcd' 1 10. The combinatiomwithagas-compressor, of an auxiliary pump provided with a means of supplying its pumping-chamber with a liq-.

whereby the liquid 5 uid under the working prcssure'of the com pressor, and arranged to admit the liquid to the chamber of the pump andscal-the piston rod of the compressor under a pressure equal to'that exerted by the compressor uponthe gas being compressed, substantially vas described;

11. The combination, with agas-comprcssor having a liquid-sealed piston-rod,'of an auxiliary pump which is provided with suitable charged with gas and the piston-rod of the compressor,

valves and conduits, whereby a scaling 0r luhricating liquid is not only introduced from said pump into the compressor and while the same is fully chargcd'with gas, but under a pressure equal to the pressure exert-ed upon the gas being compressed, substantially as de scribed.

12. The conibinatiomwith agaseompressor having a liquid-sealed piston-rod, of an auxihary pnm p which is provided with suitable valves andcouduits connecting it with said compressor, and whereby a sealing or lubricating liquid is not only introduced from said pump into the compressor and while the same is fully charged withgas, but under a pressure in excess of the pressure exerted upon the gas being compressed, substantially as described.

13. The combination,with a gas-compressor, of an auxiliary pumpprovided with suitable valves and conduits connecting it with said compressor, all constructed and operating to inject a sealing or lubricating liquid into a compressing-chamber of a compressor fully charged with gas and under a pressure equal to the pressure of the gas entering the comprcssor to be compressed, all without exposure to the atmosphere, substantially as described.

14. The combination,with a gas-compressor, of an auxiliary pump provided with suitablevalves and conduits connecting it'with said compressor, all constructed. and operating to introduce a sealing or lubricating liquid into a compressing-chambcr of a compressor fully under a pressure in excess of the prcssurc'of the gas entering the compressor to be compressed, substantially as described.

15. The combi nation,wit-h a gas-compressor, of an auxiliary pump constructed and so arranged that a liquid-zu'lmitted within a liquidchamber of said pump operates to first seal and is then discharged into the compressing-cylindcr of the gascompressor when the said compressorhas received its full complement of gas, substantially as described.

16. The combination, with a gas-compressor, of an auxiliary pump constructed, connected, and operating to admit aliquid within a, chamber of said pump, and thereby seal the piston-rod of the compressor, and then discharge said liquid into a compressing-cylinder of a gas-compressor when the latter is fully charged with gas and during the act of compression, spbstantially as described.

17. The combination, with a gas-compressor, of an auxiliary pump and connectingpipes constructed and operating to introduce a fresh. supply of cooled liquid within a cham her around the piston-rod outside of the compressor at each stroke of the piston, and seal the piston-rod orifice in the head ot the compressor on its outer side, substantially as de- 5 scribed.

18. The'comhmation, with a gas-compressor, of an auxiliary pump constructed and operating to continuously inter-pose a supply of liquid between-the head of the compressor and the outer stuiiingbox 'of its piston-rod, substantially as described.

' 19. The combination, with a gas-compressor, of an auxiliary pump constructed and opcrating to continuously circulate a fresh supply of sealing or lubricating liquid in the space inclosednot occupied by the pistonrod of the compressor-between the head of the compressor and the outer stufiing-box encircling the piston-rod of the compressor, substantially as described.

20. Thc-combiuation, with a gas-compressor, of adouble-acting liquid-supplying pump provided with suitable valves and conduits, and constructed, connected, and operating-to introduce a sealing or lubricating liquid into a chamber of the gas-compressor when the said .compressor is fully charged with gas, substantially as described.

21. The combination, with a double-acting gas-compressor, of a double-acting supplying pump having suitable valves and conduits, whereby a sealing or lubricating liquid is introduced into a chamber of the gas-compressor when the said compressor is fully charged with gas, substantially as described.

2. A. gas-compressor having an inlet-valve for the introduction of a sealing or lubricating liquid into a chamber of said compressor, which valve is provided with a piston of larger diameter and greater area than the seat of said valve, and the said valve is held in its seat by a pressure exerted upon such surface of its piston that is in excess of the pressurc. tending to raise the valve from itsseat during the suction-stroke ofthe piston, substantially as described.

23. A gascompressor having a chamber connected with or attached to the head of the said compressor, wherein a sealing or lubricating liquid seals the piston-rod oriiicein the head of said compressor on its outer side under a pressure equal to or in excess of the working pressure of the compressor, in combination with an auxiliary pump provided with suitable valves and connecting-pipes, and constructed and arranged to introduce the said liquid within a comprcssionchamber of said compressor when the latter is-fully dharged with gas, substantially as described.

24. The combinatio'mwith agas-compressor, of an auxiliary pump a liquid-supply chamber, valves controlling the same, and passages leading therefrom to its pumpirig-chamber, whereby a liquid entering the pump under the working pressure of the compressor 0peratcs to. raise the valves and alternately supply each end of the pumping-chamber with its charge of liquid upon each stroke of the compressor-piston,substantially as described.

25. A gas-compressor constructed and arranged toadmit of the introduction of a sealing or lubricating liquid into a chamber of said compressor when fully charged with gas 26. A gas-compressor constructed and ar-" ranged to admit of the introduction of a sealing or lubricating liquid into a chamber of said compressor when fully charged with gas when the said sealing or lubricating liquid is charged with gas oral-iquefied gas atapressn re in excess ofthepressure of the gas entering tne compressor to be compressed, and which liquid is introduced while under such pressure into the sa? '1 compressor, in combination with an auxiliary pump, a condenser, a reservoir for holding the sealing'or lubricating liquid, and their in ermediate connecting-pipes, substantially as described.

27. A ranged to admit of the introduction of a sealing orlubricating'liquid into a chamber of said compressor when fully charged with gas when the said sealing orlubricating liquid is charged with gas ora liquefied gas at a pressure in excess of that of the gas entering the compressor to be compressed, and which is introduced.

while under such pressure into the said coinlpressor, in combination with a gas-consenser,

a reservoir --.for holding the sealing or lubricating liquld,and a coil of pipes or a chamber wherein the liquefied gas is expanded, and their intermediate connecting-pipes, substan tially as described.

28. A gas-compressor constructed and arranged to admit of the introduction of a sealing or lubricating liquid into a chamber of said compressor when fully charged with gas when the said sealing or lubricating liquid is charged with gas or a liquefied gas ata pressure in excess of that of the gas entering the compressor to ac compressed, and which is introduced while under such pressure into the said compressor, in combination with a gascondenser, a reservoir for holding the sealing orlubricatingliquid,aliquid-supplyingpump, a coil or chamber in which the liquefied gas is expanded, and their intermediate connectingpipes, substantially as described.

29. A gas-compressor whereof the valves for controlling the introduction of the sealing or lubricating liquid are constructed and operate with relation to the vacuum or com pression chamber of said compressor to prevent the sealing or lubricating liquid under pressure from entering the compression-chamber of said compressor during the suction-stroke of the compressor-piston, substantially as described.

30. A. gas-compressor whereof the valves gas-compressor constructed and are for controlling the introduction of the sealing or lubricatingliquid are. constructed and operate with relation to the vacuum or compression chamber of said compressor to close. and prevent the sealing or lubricating liquid under pressure from entering the compressingchamber of said compressor duringithe suction-stroke of the compressor-piston, andto open and admit said liquid to the compres sion-chamber of said compressor during the act of compression, substantiallyas described.

, 31. A gas-compressor, in combination with an auxiliary pump provided with suitable valves and connecting-pipes, whereby a sealing or lubricatingliquid is introduced within a chamber outside of the cylinder of the compressor, thereby sealing the piston-rod of the compressor, substantially as described.

32. A gas-compressor, in combination with an auxiliary pump provided with suitable valves and connecting -pipes,whereby a sealing or lubricatingliquid is introduced within a chamber outside of the cylinder of the com-- pressor, which liquid seals the piston-rod of the compressor under pressure, as described.

33. The combination, with a gas-compressor and a liquid-reservoir, of connecting-pipes and a pressure device,lwhereby a sealing or lubricating liquid is introduced into the compressor under a pressure in excess of the pressure of the gas entering the compressor to be compressed, substantially as described.

34. The combination, with a gas-compressor and a liquid reservoir, of connecting-pipes and'a measuring device operating to determine the quantity of sealing or lubricating liquid introduced within the compressor,substantially as described.

35. A gas-compressor having an outside chamber for'sealing its piston-rod with a liquid, a piston-rod sealed under a pressure in excess of the gas entering the compressor, and a measuring device operating to determine the quantity of scaling or lubricating liquid introduced within the compressor, in combina' substantially tion with a liquid-reservoir and connectingpipes, substantially as described.

36. The gas-compressor B, in combination with the pump 0 and their conduits or connecting-pipes, all constructed and operating substantially as described.

37. A gas-compressor provided with the valves j and j, which have pistons of greater diameter and greater area than the said valves, the auxiliary pump C, the pipes 8, s,

', p, p, and q, and the intermediate conhecting-pipes, all in combinatiou,substantially as described.

39. A gas-compressor, in combination with. an auxiliary pump, a condensing-coil, aa-ex- 1 pansion coil,- and intermediate connectingpipes, a chamber around the piston-rod in the stufling-box of the auxiliary pump, and an inlet whereby the partially-expanded gas returnio ing to the compressor to be recompressed may be introduced into the said stuffing-box hamher and cool the piston-rod, substantially as described. W

V 40. A gas-compressor, in combination with i 5 an auxiliary pump, an expansion-coil, a con- (lensing coil,- and intermediate connectingpipes,- and a chamber of the auxiliary pump, through which the piston-rod of the compressor passes. and which chamber has communication with the expansion-coil orapipc in which the partially-expanded gasis returned to the compressor for recompression, whereby the piston-r0d of the compressor is cooled, substantially as described.

2 41. A gas-compressor, in combination with an expansion-coil, a gas-condenser, and intermediate connecting-pipes, when the said gascompressor has a piston-rod passing through a chamber communicating with a pipe on the expansion side of the appa with the partial] y-expau'ded gas, substantially as described.

42. A gas-compressor having inlets constructed and operating to admit a sealing or lubricating liquid to a chamber of the compressor in the form of spray or jets, in combination with a liquid-reservoir and connectingpipes, the whole constructed and operating to 0 circulate the said sealing or lubricating liquid and introduce the sameto the compremor without exposure to the atmosphere either prior to or during the act of compression. substantially as described. 43. Adouble actinggas-compressor,aliquidreservoir, a gas-condenser, an expansion-coil, means for introducing asealing or lubricating liquid within the said compressor during each act of compression and without exposure to the atmosphere, and connecting-pipes,'all in combination, substantially as described.

44. 1Ihe combination, with a double-acting for. collecting thelubricating or sealingliquid,

and wherein the said piston -rod is cooled by direct contact gas-mpressor, of a liquid-reservoir, means for introducing a lubricating-liquid'into each of the compression-chambers of the said compressor, either prior. to or during the act of compression and withoutoxposnre to the at mosphere, under a pressure exceeding the pressure of the gas entering the compressor to be compressed, and connecting-pipes, substantially as described.

-45. Thecon binatiomwith ages-compressor and its discharging-pipe, of acasing, as T, surrounding said pipe and forming a reservoir s substantially as described. 7

- 46. The eombinatiomwith a gas-compressor havinga liquid-sealed piston-rod,of a reservoir with liquid, connecting-pipes, and means of charging a sealing or lubricating liquid with 7 gas orliquefied gas under a pressure exceeding the pressure of the entering the com,- pressor to be comp v: all arrang'edand op.- erating to inject such. sealing or lubricating liquid while so charged with gas and while under such pressure into a chamber-of a gascompressor, substantially as described.

47. The combination,with a gas-compressor, of a means of dissolving a gas in a sealing or lubricating liquid, or charging said liquid with gas or liquefied gas under pressure, when arranged and. .operating to inject such liquid whileunder pressure and so charged with gas into the compression-chambers of a gas-compressor, substantially as described.

48. The combination, with a gas-compressor, of a means of dissolving a gas in a sealin or lubricating liquid, or charging said sealing'or lubricating liquid with gas or liquefied gas under a pressure in excess of the pressure of 0 the gas entering the compressor to be com: pressed. when arranged and operating to introduee such scaling or lubricating liquid while under such pressure and so charged with gas or liquefied gas into .a gas-compressor which has received its full charge of gas, substantially as described. In testimony whereof I have hereunto subscribed my name in the presence of two wit- JULIUS J. SUCKERT. Witnesses:

. W. L. Bmmnu, J. E. WARNER. 

